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CN112553268B - Method and device for synthesizing trehalose by ultrasound-assisted enzyme - Google Patents

Method and device for synthesizing trehalose by ultrasound-assisted enzyme Download PDF

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CN112553268B
CN112553268B CN202011246407.4A CN202011246407A CN112553268B CN 112553268 B CN112553268 B CN 112553268B CN 202011246407 A CN202011246407 A CN 202011246407A CN 112553268 B CN112553268 B CN 112553268B
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梁承�
陈成
余义发
邹林君
吴宁
邹仕刚
闭革林
吴志雄
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Nanning Harworld Biotechnology Co ltd
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Abstract

本发明涉及酶制备领域,具体公开了一种超声辅助酶合成海藻糖的方法及装置,包括以下步骤往反应釜中加入水、淀粉、α‑淀粉酶进行混合,然后调节pH值,接着加入无水氯化钙,启动反应釜的搅拌轴搅拌上述混合物、多个超声换能器、加热器和测温器,启动循环通路将反应釜底部的混合物先向外转移粉碎过滤,再送回反应釜之内;分阶段加热混合物以及保温;当液化DE值为15之后停止加热,混合物在搅拌和循环冷却至常温,调节混合物的pH值,然后加入普鲁兰酶、MTSase、MTHase和α/β‑CGTase,重新加热并在45℃下保温、调节混合物的pH值,最后加入糖化酶进行混合,最终得到产物。通过超声辅助酶促合成海藻糖,对提高以大米淀粉为基本原料合成海藻糖转化率效果明显。

The invention relates to the field of enzyme preparation, and specifically discloses a method and device for synthesizing trehalose with ultrasound-assisted enzyme, which includes the following steps: adding water, starch, and α-amylase to a reaction kettle for mixing, then adjusting the pH value, and then adding Calcium chloride water, start the stirring shaft of the reactor to stir the above mixture, multiple ultrasonic transducers, heaters and thermometers, start the circulation path to transfer the mixture at the bottom of the reactor outward, crush and filter, and then return it to the reactor. within; heat the mixture in stages and keep it warm; stop heating when the liquefied DE value reaches 15, cool the mixture to normal temperature while stirring and circulating, adjust the pH value of the mixture, and then add pullulanase, MTSase, MTHase and α/β-CGTase , reheat and keep at 45°C, adjust the pH value of the mixture, and finally add glucoamylase for mixing to finally obtain the product. Ultrasound-assisted enzymatic synthesis of trehalose has a significant effect on improving the conversion rate of trehalose synthesized from rice starch as the basic raw material.

Description

一种超声辅助酶合成海藻糖的方法及装置A method and device for ultrasonic-assisted enzymatic synthesis of trehalose

技术领域Technical field

本发明属于酶制备领域,特别涉及一种超声辅助酶合成海藻糖的方法及装置。The invention belongs to the field of enzyme preparation, and in particular relates to a method and device for synthesizing trehalose with an ultrasound-assisted enzyme.

背景技术Background technique

长年生活在沙漠地带的一些昆虫和植物,在中午的高温下几乎被干燥脱水,处在生理学上的假死状态,但一经降雨补充水分,数小时后就能复活。英国剑桥大学的学者对这些隐生生物的研究表明,这种复活现象是由于其体内存在高浓度的海藻糖。另外,一些蛙类等生物能在严寒条件下生存下来,其重要的原因也在于海藻糖对细胞的保护作用。许多生物在胁迫环境(如饥饿、高温、冷冻、干燥、高渗、辐射、有毒物质等)下表现出的抗逆耐受力与体内的海藻糖含量有直接的关系。酵母在脱去90%水分,复水后仍能复活,在长期饥饿条件下,酵母的存活率依赖于体内海藻糖的含量。有报道对酵母进行热休克和乙醇休克处理,可引起胞内海藻糖含量明显增加。Some insects and plants that have lived in the desert for many years are almost dried out and dehydrated in the high temperature at noon, and are in a state of physiological suspended animation. However, once rainfall replenishes water, they can be revived within a few hours. Research on these cryptobionts by scholars at the University of Cambridge in the UK shows that this resurrection phenomenon is due to the presence of high concentrations of trehalose in their bodies. In addition, some frogs and other organisms can survive in severe cold conditions. The important reason is also the protective effect of trehalose on cells. The stress tolerance displayed by many organisms under stressful environments (such as starvation, high temperature, freezing, drying, hypertonicity, radiation, toxic substances, etc.) is directly related to the trehalose content in the body. Yeast can still be resurrected after removing 90% of its water and rehydrating it. Under long-term starvation conditions, the survival rate of yeast depends on the trehalose content in the body. It has been reported that heat shock and ethanol shock treatment of yeast can cause a significant increase in intracellular trehalose content.

海藻糖是一种对于环境变化形成的应激状态具有高抗性的物质,是生物体内的一种典型的应激代谢物。在各种恶劣环境下,海藻糖表现出对物种的生物膜、蛋白质和核酸等生物大分子良好的保护作用。最新的研究表明,外源性的海藻糖具有良好的非特异性保护作用,因此有人把海藻糖称为“生命之糖”。Trehalose is a substance that is highly resistant to stress caused by environmental changes and is a typical stress metabolite in organisms. In various harsh environments, trehalose has shown good protective effects on species' biofilms, proteins, nucleic acids and other biological macromolecules. The latest research shows that exogenous trehalose has a good non-specific protective effect, so some people call trehalose the "sugar of life."

随着社会生活水平的提高,海藻糖的需求量在不断增大。由于海藻糖产率低、生产工艺复杂,产品价格仍然偏高,限制了海藻糖的推广应用,如何提高海藻糖产量、如何改进生产方法、如何降低生产成本是研究海藻糖的重要课题。With the improvement of social living standards, the demand for trehalose is constantly increasing. Due to the low yield of trehalose and the complicated production process, the product price is still high, which limits the promotion and application of trehalose. How to increase the yield of trehalose, how to improve the production method, and how to reduce the production cost are important topics in the research of trehalose.

发明内容Contents of the invention

本发明的目的在于提供一种超声辅助酶合成海藻糖的方法及装置,提高合成海藻糖的效率。The object of the present invention is to provide a method and device for ultrasound-assisted enzyme synthesis of trehalose to improve the efficiency of synthesizing trehalose.

为实现上述目的,本发明提供了一种超声辅助酶合成海藻糖的方法,包括以下步骤:In order to achieve the above object, the present invention provides a method for ultrasound-assisted enzyme synthesis of trehalose, which includes the following steps:

S1.往反应釜中加入水、150g/L大米淀粉、活性为15U/g的α-淀粉酶,用酸调至pH值为6.2,同时加入无水氯化钙,使最终浓度为2g/L;S1. Add water, 150g/L rice starch, and α-amylase with an activity of 15U/g into the reaction kettle, adjust the pH value to 6.2 with acid, and add anhydrous calcium chloride at the same time to make the final concentration 2g/L. ;

S2.启动反应釜的搅拌轴搅拌上述混合物,同时,启动反应釜之中被上述混合物浸没的超声换能器,超声换能器的实际功率为100-200w、振动频率为30kHz,启动反应釜内的加热器,启动循环通路将反应釜底部的混合物先向外转移粉碎过滤,再送回反应釜之内;S2. Start the stirring shaft of the reactor to stir the above mixture. At the same time, start the ultrasonic transducer in the reactor that is submerged in the above mixture. The actual power of the ultrasonic transducer is 100-200w and the vibration frequency is 30kHz. Start the ultrasonic transducer in the reactor. The heater starts the circulation path to transfer the mixture at the bottom of the reactor outward, crush, filter, and then return it to the reactor;

S3.加热混合物至75℃,当混合物的温度等于75℃后,保温若干时间,加热混合物至90℃,保温若干时间;S3. Heat the mixture to 75°C. When the temperature of the mixture equals 75°C, keep it warm for a certain period of time. Heat the mixture to 90°C and keep it warm for a certain period of time;

S4.当液化DE值为15之后停止加热,混合物在搅拌和循环冷却至常温,同时调节混合物的pH为6;S4. When the liquefaction DE value reaches 15, stop heating, stir and circulate the mixture to cool to normal temperature, and adjust the pH of the mixture to 6;

S5.加入0.75U/ml的普鲁兰酶,加入2.4U/ml的MTSase和MTHase,加入浓度为1.4U/ml的α/β-CGTase,重新加热并在45℃下保温25-30h,调节混合物的pH值为4.5;S5. Add 0.75U/ml pullulanase, add 2.4U/ml MTSase and MTHase, add α/β-CGTase with a concentration of 1.4U/ml, reheat and incubate at 45°C for 25-30h, adjust The pH of the mixture is 4.5;

S6.加入糖化酶,同时升高温度至60℃并保温10-12h;S6. Add glucoamylase, raise the temperature to 60°C and keep it incubated for 10-12 hours;

S7.得到产物。S7. Obtain the product.

作为上述方案的改进,所述MTSase通过B.subtilis/pHY300PLK-PgsiB-Y发酵而来,所述MTHase通过B.subtilis/pHY300PLK-Pxyl-Z发酵而来,所述α/β-CGTase是通过B.subtilis/pHY300PLK- PhpaII-PamyQ’-CGT发酵而来。As an improvement to the above scheme, the MTSase is fermented by B.subtilis/pHY300PLK-PgsiB-Y, the MTHase is fermented by B.subtilis/pHY300PLK-Pxyl-Z, and the α/β-CGTase is fermented by B .subtilis/pHY300PLK- Fermented from PhpaII-PamyQ'-CGT.

作为上述方案的改进,步骤S4中,打开反应釜的换气口散热,混合物在搅拌和循环中自然冷却。As an improvement to the above solution, in step S4, the ventilation port of the reaction kettle is opened to dissipate heat, and the mixture is naturally cooled during stirring and circulation.

为实现上述目的,本发明提供了一种超声辅助酶合成海藻糖的装置,包括反应釜,所述反应釜的内侧具有搅拌桨、加热器和测温器,所述反应釜的上端具有进液口及其阀门,所述反应釜的下端具有排液口及其阀门,其特征在于:所述反应釜的下端排液口设置两条分路分别为第一分路和第二分路,所述第一分路用于将混合物排至外界,所述第二分路折返回反应釜的进液口,所述第二分路上设有泵体和粉碎器,所述反应釜的侧壁设有若干超声换能器,各个所述超声换能器的发射端朝向反应釜的内侧。In order to achieve the above object, the present invention provides a device for ultrasonic-assisted enzymatic synthesis of trehalose, which includes a reaction kettle. The inside of the reaction kettle is provided with a stirring paddle, a heater and a thermometer, and the upper end of the reaction kettle is provided with a liquid inlet. The lower end of the reaction kettle has a drain port and a valve thereof. The lower end of the reaction kettle has a drain port and a valve thereof. The characteristic is that the drain port at the lower end of the reactor is provided with two branches, namely the first branch and the second branch. The first branch is used to discharge the mixture to the outside world, the second branch returns to the liquid inlet of the reaction kettle, the second branch is provided with a pump body and a pulverizer, and the side wall of the reaction kettle is provided with There are several ultrasonic transducers, and the transmitting end of each ultrasonic transducer faces the inside of the reactor.

作为上述方案的改进,所述第二分路在避开粉碎器的位置设置第三分路及其阀门,用于通过不需要进一步粉碎的混合物。As an improvement to the above solution, the second branch is provided with a third branch and its valve at a position away from the pulverizer, for passing the mixture that does not require further pulverization.

作为上述方案的改进,所述第二分路上设有取样口。As an improvement to the above solution, a sampling port is provided on the second branch road.

作为上述方案的改进,所述搅拌桨的叶片为螺旋叶片,在所述搅拌桨旋转时,螺旋叶片带动混合物上升,混合物从反应釜靠近内侧的位置下降。As an improvement to the above solution, the blades of the stirring paddle are spiral blades. When the stirring paddle rotates, the spiral blades drive the mixture to rise, and the mixture descends from a position near the inside of the reaction kettle.

本发明具有如下有益效果:The invention has the following beneficial effects:

1、采用超声波辅助酶促合成海藻糖方法,有效提高了海藻糖转化率,节约了资源,降低成本,并且海藻糖产量高,利于工业生产应用。1. The ultrasonic-assisted enzymatic synthesis of trehalose effectively improves the trehalose conversion rate, saves resources, reduces costs, and has high trehalose yield, which is conducive to industrial production and application.

2、淀粉液化和酶催化合成反应,在同一反应釜中进行,省去了物料转移的麻烦,节省劳动时间,提高效率。2. Starch liquefaction and enzyme-catalyzed synthesis reactions are carried out in the same reactor, eliminating the trouble of material transfer, saving labor time and improving efficiency.

3、采取超微粉碎和物料循环流动条件下,淀粉液化,液化效率提高,加热、冷却均匀,浆料可上下循化流动,不存在搅拌死角。3. Under the conditions of ultra-fine grinding and material circulation, the starch is liquefied, the liquefaction efficiency is improved, heating and cooling are uniform, the slurry can circulate up and down, and there is no mixing dead zone.

附图说明Description of the drawings

图1是一种实施例下反应釜及内部的结构图。Figure 1 is a structural diagram of a reactor and its interior under an embodiment.

附图标记说明:10、反应釜;11、进液口;21、排液口;13、搅拌桨;14、加热器;15、测温器;16、超声换能器;21、泵体;22、粉碎器;31、第一分路;32、第二分路;33、第三分路;34、取样口。Explanation of reference signs: 10. Reactor; 11. Liquid inlet; 21. Liquid outlet; 13. Stirring paddle; 14. Heater; 15. Thermometer; 16. Ultrasonic transducer; 21. Pump body; 22. Crusher; 31. First branch; 32. Second branch; 33. Third branch; 34. Sampling port.

具体实施方式Detailed ways

下面结合附图,对本发明的具体实施方式进行详细描述,但应当理解本发明的保护范围并不受具体实施方式的限制。The specific embodiments of the present invention will be described in detail below with reference to the accompanying drawings, but it should be understood that the protection scope of the present invention is not limited by the specific embodiments.

参照图1,本发明公开了一种超声辅助酶合成海藻糖的方法及装置。Referring to Figure 1, the present invention discloses a method and device for ultrasound-assisted enzymatic synthesis of trehalose.

装置以现有的反应釜10为基础,所述反应釜10的内侧具有搅拌桨13、加热器14和测温器15,所述反应釜10的上端具有进液口11及其阀门,所述反应釜10的下端具有排液口12及其阀门。进一步,所述反应釜10的下端排液口12设置两条分路分别为第一分路31和第二分路32,所述第一分路31用于将混合物排至外界,所述第二分路32折返回反应釜10的进液口11,所述第二分路32上设有泵体21和粉碎器22,所述反应釜10的侧壁设有若干超声换能器16,各个所述超声换能器16的发射端朝向反应釜10的内侧。图1中的箭头表示混合物的流动方向,混合物在反应釜10内搅拌后,被泵体21驱动沿左侧的第二分路32折返回进液口11,如此再重新投入反应釜10。The device is based on the existing reaction kettle 10. The inside of the reaction kettle 10 has a stirring paddle 13, a heater 14 and a thermometer 15. The upper end of the reaction kettle 10 has a liquid inlet 11 and its valve. The lower end of the reaction kettle 10 has a drain port 12 and its valve. Furthermore, the lower end drain port 12 of the reaction kettle 10 is provided with two branches, namely a first branch 31 and a second branch 32. The first branch 31 is used to discharge the mixture to the outside, and the third branch is used to discharge the mixture to the outside. The second branch 32 returns to the liquid inlet 11 of the reaction kettle 10. The second branch 32 is provided with a pump body 21 and a pulverizer 22. The side wall of the reaction kettle 10 is provided with a number of ultrasonic transducers 16. The transmitting end of each ultrasonic transducer 16 faces the inside of the reactor 10 . The arrows in Figure 1 indicate the flow direction of the mixture. After the mixture is stirred in the reaction kettle 10, it is driven by the pump 21 and returns to the liquid inlet 11 along the second branch 32 on the left, and then is put back into the reaction kettle 10.

本实施例中,反应釜10的侧壁钻若干个孔用于插入若干个超声换能器16,然后反应釜10的内侧做好密封,在缝隙处设置密封圈。各个超声换能器16均匀分布,提供均匀地振动,各个超声换能器16的导线、信号线均连接计算机。加热器14为加热棒,悬置或固定在反应釜10内即可。In this embodiment, several holes are drilled in the side wall of the reaction kettle 10 for inserting several ultrasonic transducers 16, and then the inside of the reaction kettle 10 is sealed, and a sealing ring is provided at the gap. Each ultrasonic transducer 16 is evenly distributed to provide uniform vibration, and the wires and signal lines of each ultrasonic transducer 16 are connected to the computer. The heater 14 is a heating rod, which can be suspended or fixed in the reaction kettle 10 .

作为优选,所述第二分路32在避开粉碎器22的位置设置第三分路33及其阀门,用于通过不需要进一步粉碎的混合物。本实施例中,粉碎器22为盘式超微高速剪切粉碎机。如果混合物已经足够细小,则可以不经过粉碎器22;此时所述第二分路32在避开粉碎器22的位置设置第三分路33及其阀门,图1中可以看到第三分路33的起点在粉碎器22之前,第三分路33的终点在粉碎器22之后。Preferably, the second branch 32 is provided with a third branch 33 and its valve at a position away from the pulverizer 22 for passing the mixture that does not require further pulverization. In this embodiment, the pulverizer 22 is a disk-type ultra-fine high-speed shear pulverizer. If the mixture is fine enough, it does not need to pass through the pulverizer 22; at this time, the second branch 32 is provided with a third branch 33 and its valve at a position avoiding the pulverizer 22. The third branch 33 can be seen in Figure 1 The starting point of the path 33 is before the pulverizer 22 , and the end point of the third branch path 33 is after the pulverizer 22 .

作为优选,所述第二分路32上设有取样口34,如此可以清楚地监测反应釜10内混合物的反应状况。Preferably, the second branch 32 is provided with a sampling port 34 so that the reaction status of the mixture in the reactor 10 can be clearly monitored.

作为优选,所述搅拌桨13的叶片为螺旋叶片,在所述搅拌桨13旋转时,螺旋叶片带动混合物上升,混合物从反应釜10靠近内侧的位置下降。图1中标识的箭头表示混合物的流动状态,位于反应釜10中间的混合物被螺旋叶片牵引,而位于反应釜10边缘的混合物自然下降。如此可以保证物料与酶在反应过程中的均一性,消除物料与酶内部的温度梯度,从而提高反应速度和反应效率。Preferably, the blades of the stirring paddle 13 are spiral blades. When the stirring paddle 13 rotates, the spiral blades drive the mixture to rise, and the mixture descends from a position close to the inside of the reaction kettle 10 . The arrows marked in Figure 1 represent the flow state of the mixture. The mixture located in the middle of the reactor 10 is pulled by the spiral blades, while the mixture located at the edge of the reactor 10 naturally descends. This can ensure the uniformity of the material and enzyme during the reaction process, eliminate the temperature gradient within the material and enzyme, thereby improving the reaction speed and reaction efficiency.

作为优选,测温器15为热电偶温度计。Preferably, the thermometer 15 is a thermocouple thermometer.

方法包括以下步骤:、The method includes the following steps:,

S1.往反应釜10中加入水、150g/L大米淀粉、活性为15U/g的α-淀粉酶,用酸调至pH值为6.2,同时加入无水氯化钙,使最终浓度为2g/L。S1. Add water, 150g/L rice starch, and α-amylase with an activity of 15U/g into the reaction kettle 10, adjust the pH value to 6.2 with acid, and add anhydrous calcium chloride at the same time to make the final concentration 2g/g. L.

S2.启动反应釜10的搅拌轴搅拌上述混合物,同时,启动反应釜10之中被上述混合物浸没的超声换能器16,超声换能器16的实际功率为100-200w、振动频率为30kHz,启动反应釜10内的加热器14,启动循环通路将反应釜10底部的混合物先向外转移粉碎过滤,再送回反应釜10之内。S2. Start the stirring shaft of the reactor 10 to stir the above mixture. At the same time, start the ultrasonic transducer 16 in the reactor 10 that is submerged in the above mixture. The actual power of the ultrasonic transducer 16 is 100-200w and the vibration frequency is 30kHz. The heater 14 in the reaction kettle 10 is started, the circulation path is started, and the mixture at the bottom of the reaction kettle 10 is first transferred outward, crushed, filtered, and then returned to the reaction kettle 10 .

S3.加热混合物至75℃,当混合物的温度等于75℃后,保温15min,加热混合物至90℃,保温等待液化DE值变化。为了确保加热过程的稳定,在75℃以下,按2℃/min的速率加热,在75℃以上,按3℃/min的速率加热。S3. Heat the mixture to 75°C. When the temperature of the mixture equals 75°C, keep it warm for 15 minutes. Heat the mixture to 90°C and keep it warm until the DE value of liquefaction changes. In order to ensure the stability of the heating process, the heating rate is 2°C/min below 75°C, and the heating rate is 3°C/min above 75°C.

S4.当液化DE值为15之后停止加热,混合物在搅拌和循环冷却至常温(混合物冷却时可以采用敞开自然冷却,也可以插入制冷棒),同时调节混合物的pH为6.0。S4. Stop heating when the liquefied DE value reaches 15, and the mixture is cooled to normal temperature while stirring and circulating (when the mixture is cooled, open natural cooling can be used, or a cooling rod can be inserted), and the pH of the mixture is adjusted to 6.0.

S5.加入0.75U/ml的普鲁兰酶,加入2.4U/ml的MTSase和MTHase,加入浓度为1.4U/ml的α/β-CGTase,重新加热并在45℃下保温25-30h,调节混合物的pH值为4.5。S5. Add 0.75U/ml pullulanase, add 2.4U/ml MTSase and MTHase, add α/β-CGTase with a concentration of 1.4U/ml, reheat and incubate at 45°C for 25-30h, adjust The pH of the mixture is 4.5.

S6.加入糖化酶,同时升高温度至60℃并保温10-12h。S6. Add glucoamylase, raise the temperature to 60°C and keep it incubated for 10-12 hours.

S7.得到产物。S7. Obtain the product.

上文提到的B.subtilis/pHY300PLK-PgsiB-Y、B.subtilis/pHY300PLK-Pxyl-Z和B.subtilis/pHY300PLK- PhpaII-PamyQ’-CGT均来之江南大学食品科学与技术国家重点实验室。The B.subtilis/pHY300PLK-PgsiB-Y, B.subtilis/pHY300PLK-Pxyl-Z and B.subtilis/pHY300PLK-PhpaII-PamyQ'-CGT mentioned above are all from the State Key Laboratory of Food Science and Technology, Jiangnan University .

MTSase、MTHase、α/β-CGTase的发酵方法为:The fermentation methods of MTSase, MTHase and α/β-CGTase are:

挑取单菌落于液体LB(含新霉素20ug/ml)培养 8-10h,按5%接种量将种子液转接到TB培养基(含新霉素20ug/ml)中,在37℃摇床中培养2.5h后,继续在33℃摇床培养48h左右。将发酵液于4℃、8000r/min 离心15min收集菌体,浓缩破壁得到粗酶液。Pick a single colony and culture it in liquid LB (containing neomycin 20ug/ml) for 8-10 hours. Transfer the seed liquid to TB medium (containing neomycin 20ug/ml) according to 5% inoculum volume and shake at 37°C. After culturing in the bed for 2.5 hours, continue culturing on a shaking table at 33°C for about 48 hours. The fermentation broth was centrifuged at 4°C and 8000 r/min for 15 min to collect the bacterial cells, and the cells were concentrated and broken down to obtain crude enzyme solution.

对于培养基:For culture medium:

LB液体培养基:酵母粉为5.0g,蛋白胨为10.0g,氯化钠为10.0g;LB liquid medium: yeast powder is 5.0g, peptone is 10.0g, sodium chloride is 10.0g;

LB固体培养基:将1.5~2.0g 的琼脂糖加入到100ml的LB液体培养基中;LB solid culture medium: Add 1.5 to 2.0 g of agarose to 100 ml of LB liquid culture medium;

TB培养基:蛋白胨为12.0g,酵母粉为24.0g,甘油为5.0g,KH2PO4 为2.31g,K2HPO4•3H2O为16.43g。TB medium: peptone is 12.0g, yeast powder is 24.0g, glycerol is 5.0g, KH 2 PO 4 is 2.31g, K 2 HPO 4 •3H 2 O is 16.43g.

以上述步骤为基础,对比实例取消超声换能器16,其他地方未做变动,得到产物的转换率为71.4%。Based on the above steps, the ultrasonic transducer 16 was eliminated in the comparative example, and no other changes were made, resulting in a product conversion rate of 71.4%.

以上述步骤为基础,实施例1将超声换能器16的实际频率定为100w,其他地方未做变动,得到产物的转换率为81.6%。Based on the above steps, in Example 1, the actual frequency of the ultrasonic transducer 16 is set to 100w, and other parts are not changed, and the conversion rate of the product is 81.6%.

以上述步骤为基础,实施例2将超声换能器16的实际频率定为150w,其他地方未做变动,得到产物的转换率为82.1%。Based on the above steps, in Example 2, the actual frequency of the ultrasonic transducer 16 is set to 150w, and other parts are not changed, and the conversion rate of the product is 82.1%.

以上述步骤为基础,实施例2将超声换能器16的实际频率定为150w,其他地方未做变动,得到产物的转换率为82.3%。Based on the above steps, in Example 2, the actual frequency of the ultrasonic transducer 16 is set to 150w, and other parts are not changed, and the conversion rate of the product is 82.3%.

由此可知,通过超声辅助酶促合成海藻糖,对提高以大米淀粉为基本原料合成海藻糖转化率效果明显。It can be seen that the ultrasonic-assisted enzymatic synthesis of trehalose has a significant effect on improving the conversion rate of trehalose synthesized from rice starch as the basic raw material.

前述对本发明的具体示例性实施方案的描述是为了说明和例证的目的。这些描述并非想将本发明限定为所公开的精确形式,并且很显然,根据上述教导,可以进行很多改变和变化。对示例性实施例进行选择和描述的目的在于解释本发明的特定原理及其实际应用,从而使得本领域的技术人员能够实现并利用本发明的各种不同的示例性实施方案以及各种不同的选择和改变。本发明的范围意在由权利要求书及其等同形式所限定。The foregoing descriptions of specific exemplary embodiments of the present invention have been presented for purposes of illustration and illustration. These descriptions are not intended to limit the invention to the precise form disclosed, and obviously many modifications and variations are possible in light of the above teachings. The exemplary embodiments were chosen and described in order to explain certain principles of the invention and its practical applications, thereby enabling others skilled in the art to make and utilize various exemplary embodiments of the invention and various different applications. Choice and change. The scope of the invention is intended to be defined by the claims and their equivalents.

Claims (2)

1.一种超声辅助酶合成海藻糖的方法,其特征在于包括以下步骤:1. A method for ultrasound-assisted enzymatic synthesis of trehalose, characterized by comprising the following steps: S1.往反应釜中加入水、150g/L大米淀粉、活性为15U/g的α-淀粉酶,用酸调至pH值为6.2,同时加入无水氯化钙,使最终浓度为2g/L;S1. Add water, 150g/L rice starch, and α-amylase with an activity of 15U/g into the reaction kettle, adjust the pH value to 6.2 with acid, and add anhydrous calcium chloride at the same time to make the final concentration 2g/L. ; S2.启动反应釜的搅拌轴搅拌上述混合物,同时,启动反应釜之中被上述混合物浸没的超声换能器,超声换能器的实际功率为100-200w、振动频率为30kHz,启动反应釜内的加热器,启动循环通路将反应釜底部的混合物先向外转移粉碎过滤,再送回反应釜之内;S2. Start the stirring shaft of the reactor to stir the above mixture. At the same time, start the ultrasonic transducer in the reactor that is submerged in the above mixture. The actual power of the ultrasonic transducer is 100-200w and the vibration frequency is 30kHz. Start the ultrasonic transducer in the reactor. The heater starts the circulation path to transfer the mixture at the bottom of the reactor outward, crush, filter, and then return it to the reactor; S3.加热混合物至75℃,当混合物的温度等于75℃后,保温若干时间,加热混合物至90℃,保温若干时间;S3. Heat the mixture to 75°C. When the temperature of the mixture equals 75°C, keep it warm for a certain period of time. Heat the mixture to 90°C and keep it warm for a certain period of time; S4.当液化DE值为15之后停止加热,混合物在搅拌和循环冷却至常温,同时调节混合物的pH为6;S4. When the liquefaction DE value reaches 15, stop heating, stir and circulate the mixture to cool to normal temperature, and adjust the pH of the mixture to 6; S5.加入0.75U/ml的普鲁兰酶,加入2.4U/ml的MTSase和MTHase,加入浓度为1.4U/ml的α/β-CGTase,重新加热并在45℃下保温25-30h,调节混合物的pH值为4.5;S5. Add 0.75U/ml pullulanase, add 2.4U/ml MTSase and MTHase, add α/β-CGTase with a concentration of 1.4U/ml, reheat and incubate at 45°C for 25-30h, adjust The pH of the mixture is 4.5; S6.加入糖化酶,同时升高温度至60℃并保温10-12h;S6. Add glucoamylase, raise the temperature to 60°C and keep it incubated for 10-12 hours; S7.得到产物;S7. Obtain the product; MTSase、MTHase、α/β-CGTase的发酵方法为:The fermentation methods of MTSase, MTHase and α/β-CGTase are: 挑取单菌落于液体LB含新霉素20ug/ml培养8-10h,按5%接种量将种子液转接到TB培养基含新霉素20ug/ml中,在37℃摇床中培养2.5h后,继续在33℃摇床培养48h;将发酵液于4℃、8000r/min离心15min收集菌体,浓缩破壁得到粗酶液;Pick a single colony and culture it in liquid LB containing neomycin 20ug/ml for 8-10 hours. Transfer the seed liquid to TB culture medium containing neomycin 20ug/ml according to 5% inoculation volume and culture it in a 37°C shaker for 2.5 hours. After h, continue to culture in a shaking table at 33°C for 48h; centrifuge the fermentation broth at 4°C, 8000r/min for 15min to collect the cells, concentrate and break the walls to obtain crude enzyme solution; 对于培养基:For culture medium: LB液体培养基:酵母粉为5.0g,蛋白胨为10.0g,氯化钠为10.0g;LB liquid medium: yeast powder is 5.0g, peptone is 10.0g, sodium chloride is 10.0g; LB固体培养基:将1.5~2.0g的琼脂糖加入到100ml的LB液体培养基中;LB solid culture medium: Add 1.5 to 2.0 g of agarose to 100 ml of LB liquid culture medium; TB培养基:蛋白胨为12.0g,酵母粉为24.0g,甘油为5.0g,KH2PO4为2.31g,K2HPO4·3H2O为16.43g。TB medium: peptone is 12.0g, yeast powder is 24.0g, glycerol is 5.0g, KH2PO4 is 2.31g, K2HPO4·3H2O is 16.43g. 2.根据权利要求1所述超声辅助酶合成海藻糖的方法,其特征在于:步骤S4中,打开反应釜的换气口散热,混合物在搅拌和循环中自然冷却。2. The method of ultrasonic-assisted enzyme synthesis of trehalose according to claim 1, characterized in that: in step S4, the ventilation port of the reaction kettle is opened to dissipate heat, and the mixture is naturally cooled during stirring and circulation.
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